Dynamic modeling and simulation of heavy paraffin dehydrogenation reactor for selective olefin production in linear alkyl benzene production plant

Applied Catalysis A: General

Volumn 358, Issue 1, 2009, Pages 1-6

  Zahedi, G ^a   Yaqubi, H ^a   Ba Shammakh, M ^b  

^a RAZI UNIVERSITY   (Iran)

^b KING FAHD UNIVERSITY OF PETROLEUM AND MINERALS   (Saudi Arabia)

Author keywords

Dehydrogenation; Fixed bed reactor; Linear alkyl benzene; Modeling; Paraffin

Indexed keywords

ALKYLATION; BENZENE; DEHYDROGENATION; GAS PRODUCERS; OLEFINS; ORDINARY DIFFERENTIAL EQUATIONS; PARAFFIN WAXES; PARAFFINS; PARTIAL DIFFERENTIAL EQUATIONS; PLATINUM; SURFACE REACTIONS; TIN; VEHICULAR TUNNELS;

ALGEBRAIC EQUATIONS; APPLYING PRESSURES; DETAILED MODELS; DYNAMIC MODELING AND SIMULATIONS; FIXED BED REACTOR; FUNCTION OF TIME; INDUSTRIAL REACTORS; LINEAR ALKYL BENZENE; MASS BALANCES; MASS-BALANCE EQUATIONS; MODELING; MODELING RESULTS; MOLE PERCENTS; MOMENTUM BALANCES; NUMERICAL SOLUTIONS; OLEFIN PRODUCTIONS; PRODUCTION PLANTS; REACTOR MODELS; REACTOR PERFORMANCE;

HYDROGEN PRODUCTION;

EID: 61849141756     PISSN: 0926860X     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.apcata.2009.01.043     Document Type: Article

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